EP3846921A1 - Verfahren zum betreiben einer temperaturwechseladsorptionsanlage und temperaturwechseladsorptionsanlage - Google Patents
Verfahren zum betreiben einer temperaturwechseladsorptionsanlage und temperaturwechseladsorptionsanlageInfo
- Publication number
- EP3846921A1 EP3846921A1 EP19768713.0A EP19768713A EP3846921A1 EP 3846921 A1 EP3846921 A1 EP 3846921A1 EP 19768713 A EP19768713 A EP 19768713A EP 3846921 A1 EP3846921 A1 EP 3846921A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- adsorption
- cycle
- gas mixture
- operated
- units
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 196
- 238000000034 method Methods 0.000 title claims abstract description 41
- 239000000203 mixture Substances 0.000 claims abstract description 109
- 230000008929 regeneration Effects 0.000 claims abstract description 58
- 238000011069 regeneration method Methods 0.000 claims abstract description 58
- 239000003463 adsorbent Substances 0.000 claims abstract description 43
- 238000001816 cooling Methods 0.000 claims abstract description 23
- 238000010438 heat treatment Methods 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 9
- 238000010926 purge Methods 0.000 claims description 9
- 238000011010 flushing procedure Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 230000004888 barrier function Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 90
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000003795 desorption Methods 0.000 description 3
- 239000013529 heat transfer fluid Substances 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000000274 adsorptive effect Effects 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000012432 intermediate storage Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0462—Temperature swing adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0438—Cooling or heating systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40007—Controlling pressure or temperature swing adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/403—Further details for adsorption processes and devices using three beds
Definitions
- the invention relates to a method for separating a gas mixture stream by means of temperature swing adsorption and a temperature swing adsorption system set up to carry out such a method according to the respective
- Temperature swing adsorption is an adsorptive process for the separation of gas mixtures, in which the adsorbent used is regenerated using thermal energy. Temperature swing adsorption is used, for example, for exhaust gas purification or for the preparation of gas mixtures such as natural gas or synthesis gas. Other gas mixtures can also be separated in a corresponding manner by means of temperature swing adsorption, for example gas mixtures such as biogas or exhaust gases from chemical or physical gas scrubbing processes such as the rectisol or
- Amine wash provided that their composition is suitable for a corresponding separation.
- the present invention is not limited to the use of certain adsorbents or gas mixtures.
- the temperature swing adsorption takes advantage of the temperature dependence of adsorption processes.
- An adsorbent that is in a suitable
- Adsorber container (here referred to as "adsorption unit”) is housed in an operating cycle at a lower temperature level with the gas mixture stream to be separated and thereby loaded with the component or components to be separated from the gas mixture stream.
- the operating cycle is also referred to below as the "adsorption cycle".
- the adsorbent can then be heated, i.e.
- This operating cycle is also referred to below as the "regeneration cycle".
- a Temperature swing adsorption system are therefore required at least two adsorption units so that the gas mixture stream to be separated always flows through one of the adsorption units and thus to separate the
- the temperature change adsorption can in particular in material systems
- Components are used that have high enthalpies of adsorption.
- the cycle times of the operating cycles explained are generally several hours.
- Temperature swing adsorption is generally used to remove low-concentration components in gas mixtures and is typically less suitable for removing higher-concentration components.
- the regeneration gas can be, for example, a purified process product, water vapor or nitrogen.
- the use of other regeneration gases is also possible.
- indirect heating of the adsorbent for regeneration can also be carried out in the regeneration cycle.
- a heated fluid flow can also be used for this purpose, however, for example by means of
- Heating lines through the adsorbent or an adsorber bed is guided.
- a corresponding fluid is also referred to here as a "heat transfer fluid”.
- heat transfer fluid is therefore a liquid or a gas which is passed through a separate flow channel during indirect heating and / or cooling of an adsorber and in this way is subjected to indirect heat exchange with the adsorbent.
- Temperature swing adsorption systems can be used, for example, water, thermal oil, steam or hot nitrogen.
- a corresponding adsorption unit is still desorbed with regeneration gas and a part when using a regeneration gas
- the object of the present invention is to avoid corresponding losses when rinsing an adsorption unit, if possible. Disclosure of the invention
- the present invention proposes a method for separating a gas mixture stream by means of temperature swing adsorption and one for
- Component mixtures can be enriched or depleted in one or more components in the language used here, these terms refer to a corresponding content in another component mixture, using which the component mixture under consideration was formed.
- a mixture of components is according to that used here
- pressure level and "temperature level” to characterize pressures and temperatures, which is intended to express that corresponding pressures and temperatures in a corresponding system are not in the form of exact pressure or temperature values must be used to implement the inventive concept.
- pressures and temperatures typically move in certain ranges, the maximum and minimum values of which differ by no more than 1%, 5%, 10%, 20% or even 50%, for example.
- pressure levels and temperature levels can lie in disjoint areas or in areas that overlap one another.
- pressure levels include, for example, unavoidable or expected pressure drops.
- temperature levels include, for example, unavoidable or expected pressure drops.
- the adsorption units are each at least partially filled with adsorbent, for example in the form of granules or moldings. If "three" adsorption units are referred to in simplified form below, it goes without saying that more than three adsorption units can also be present or used in a system according to the invention or a corresponding method, without this being explicitly stated.
- the three adsorption units used in the context of the present invention are operated at a time offset from one another in each case in an adsorption cycle, then in an additional cycle, then in a regeneration cycle, then in a rinsing cycle and then in a cooling cycle.
- the adsorption cycle, the additional cycle, the regeneration cycle, the rinsing cycle and the cooling cycle follow one another in the specified sequence, the specified cycles being used only in the specified sequence, but other operating cycles can be interposed between these cycles.
- a first gas mixture at a first temperature level is passed over an adsorbent in the adsorption units and components of the first gas mixture are adsorbed by the adsorbent.
- a gas mixture depleted of the components adsorbing on the adsorbent hereinafter referred to as the "second" gas mixture.
- Adsorbing components can be product components
- Act gas mixture the second gas mixture being a product mixture.
- it can also be such components that are themselves in one
- Components contained in the gas mixture must be adsorbed by the adsorbent.
- the adsorbed portion thereof depends in particular on the respective adsorption properties and the adsorbent used as well as the
- the adsorption units (as explained below in a direct or indirect manner) are heated to a second temperature level above the first temperature level and the components adsorbed by the adsorbent in the adsorption mode are at least partially desorbed by the latter.
- the desorbed components can be removed from the corresponding ones during the entire regeneration cycle or in a subsequent emptying cycle
- Adsorption units are executed. In all cases, however, a certain proportion of the desorbed components remain in the gas phase in the correspondingly regenerated adsorption units.
- Adsorption units existing (remaining) components at least partially flushed out using a purge gas (hereinafter referred to as "third" gas mixture) to obtain a loaded purge gas (hereinafter referred to as "fourth" gas mixture).
- the fourth gas mixture is a fluid that contains the desorbed components and the components of the third gas mixture. Especially when the desorbed components are
- the adsorption units are finally cooled from the second or in any case from a higher temperature level, in particular at least partially to the first temperature level.
- "At least partial" cooling means in particular cooling to the first
- Temperature level or understood to a temperature level between the first and the second temperature level.
- the present invention proposes periodically repeating first
- Adsorption units operated in the adsorption cycle one of the adsorption units in the rinsing cycle and one of the adsorption units in the additional cycle. It goes without saying that during the successive first operating periods, each of the other adsorption units is operated in the adsorption cycle, in the rinsing cycle and in the additional cycle, as will be explained in detail below.
- part of the second gas mixture is fed to the adsorption unit operated in the flushing cycle as the third gas mixture or as part of the third gas mixture, and that the fourth gas mixture or part of the fourth gas mixture is supplied in the additional cycle operated adsorption unit is supplied.
- Gas mixture contained in the regeneration cycle desorbed from the adsorbent components can in this way in the operated in the additional cycle
- Adsorption unit can be recovered in a particularly advantageous manner.
- the peculiarity of the method proposed according to the invention consists in a recycling step, as has just been explained.
- part of the second gas mixture is used as the or as part of the third gas mixture for purging the adsorption unit to be purged after the regeneration cycle, and the exiting gas stream, the fourth gas mixture, is again fed to an adsorption, specifically in the operated in the additional clock
- the escaping gas from the purged adsorption unit i.e. the fourth gas mixture, contains a higher concentration of each components to be separated (or has a higher partial pressure of these
- the loading of the adsorbent can be increased. It is precisely this process control that allows the adsorbent to be better utilized in the context of the present invention and a large part of the product used for rinsing to be recovered. The amount of gas withdrawn for purging can be almost completely compensated in this way.
- Adsorption units can be achieved without a corresponding return. Overall, the yield of the respective target component can in particular be significantly increased in the context of the present invention.
- a blower can be used to compensate for the pressure drop across the adsorbers operated in the additional cycle or in the other cycles mentioned.
- Adsorption units can be found that here the fourth gas mixture at least partially at the first temperature level via an adsorbent in the
- a fifth gas mixture obtained in this way is at least partially fed to the second gas mixture.
- the fifth gas mixture is depleted of those adsorbing from the adsorbent
- Adsorption units operated in the cooling cycle The previously explained first and second operating periods are explained in more detail below, in particular with reference to FIGS. 1 and 2.
- a portion of the second gas mixture obtained in the adsorption cycle can also be used for cooling in the second operating periods. For this purpose, this can be introduced into a corresponding adsorption unit. In this way, the pressure can be maintained in a corresponding adsorption unit. Without this measure, the pressure could drop, which could have a negative impact on the performance in the subsequent adsorption step.
- adsorption units operated in the cycles mentioned alternate with each instance in the first.
- that adsorption unit is operated in the adsorption cycle in the first operating periods, that in a first one preceding the time
- a "temporally preceding" first operating period denotes the previous first operating period, with no further first operating period lying between this temporally preceding and the respectively considered first operating period.
- Regeneration cycle take place in that a fluid is passed through the adsorption unit operated in the regeneration cycle and comes into material contact with the adsorbent in the adsorption unit. Using an appropriate fluid
- the regeneration cycle can also be subdivided and a gas mixture removed from the adsorption unit operated in the regeneration cycle can be partially supplied to the adsorption unit operated in the additional cycle. This can be the case in particular when the majority of these components have already been desorbed and a corresponding residual gas no longer has an effectively usable fraction of these components.
- Gas mixture can be taken from the system as a product gas mixture or the components which are at least partially adsorbed in the regeneration cycle can be converted into a corresponding product gas mixture.
- the respective target component can be the weakly adsorbing component, but also the more strongly adsorbing component, which can be found in the product or in the residual gas in this way.
- the third gas mixture can be preheated before it is used in the flushing cycle. In this way, the
- Adsorption unit Gas mixture or the part thereof, which of the operated in the additional stroke Adsorption unit is supplied to cool at least partially.
- the adsorption in the additional cycle on the adsorbent used can be improved due to the temperature drop.
- a corresponding buffer container which can be used for the intermediate storage of the third gas mixture and thus the residual gas, can also be operated in a pressure change, so that an increased storage capacity results. In this way, a so-called "residual gas hole" can be filled by the discontinuous residual gas.
- the first can within the scope of the present invention
- Temperature level that is, the temperature level of the adsorption, at 15 to 50 ° C.
- the second temperature level can be, for example, 100 to 300 ° C.
- the operating pressures used depend in particular on the respective
- Operation area They are typically between 10 and 100 bar absolute pressure.
- the present invention also extends to
- Temperature swing adsorption system which can be set up, in particular, for operation according to a method as was explained above in embodiments.
- Temperature swing adsorption system which can be set up, in particular, for operation according to a method as was explained above in embodiments.
- A denotes an adsorption cycle
- Z an additional cycle
- R a regeneration cycle
- S a rinsing cycle
- K a cooling cycle
- FIG. 1 illustrates a method according to an embodiment of the invention in the form of a simplified process diagram.
- Figure 2 illustrates a method according to an embodiment of the invention in the form of a simplified process diagram.
- FIG. 1 shows a method according to an embodiment of the present invention in the form of a simplified process diagram. At the same time, FIG. 1 shows a corresponding system, which is designated 100 in total. In the method or system 100 illustrated in FIG. 1 there are three
- Adsorption units 1, 2, 3 are provided or are used accordingly.
- Figure 1 illustrates an instance of a first operating period (see also 1 .1 in Table 1), as previously explained in detail.
- the three adsorption units are shown in the example shown in an adsorption cycle (A, adsorption unit 1), in an additional cycle (Z, adsorption unit 2) and a rinsing cycle (S,
- Adsorption unit 3 operated. In the following first operating periods, as illustrated in Table 1, the system switches continuously.
- the adsorption unit 1 located in the adsorption cycle A is fed a first gas mixture a at a first temperature level.
- a second gas mixture b is obtained, components of the first gas mixture a adsorbing on an adsorbent in the adsorption unit 1.
- the second gas mixture b can be used to provide a product mixture p.
- the adsorption unit 2 is in the additional cycle Z, the adsorption unit 3 in the rinsing cycle S. In the rinsing cycle S are not illustrated in one
- Regeneration cycle (R, see Figure 2) desorbed and after
- the regeneration cycle of the components present in the adsorption unit 1 is at least partially rinsed out by means of a third gas mixture, which is denoted here by c, and to obtain a fourth gas mixture, denoted here by d.
- a third gas mixture which is denoted here by c
- a fourth gas mixture denoted here by d.
- part of the second gas mixture b is fed to the adsorption unit 3 operated in the flushing cycle S as part of the third gas mixture c.
- the fourth gas mixture d is fed to the adsorption unit 2 operated in the additional cycle Z, the adsorbable components also adsorbing here.
- a fifth gas mixture e is obtained, which in the example shown is at least partially combined with the second gas mixture b.
- FIG. 2 illustrates the previously mentioned several times and as "second"
- Operating period is the operating period in one instance (see also 2.1 in Table 1).
- the first adsorption unit 1 is located therein in the adsorption cycle A, the second adsorption unit 2 in a regeneration cycle R and the third
- Adsorption unit 3 in a cooling cycle K Adsorption unit 3 in a cooling cycle K.
- the adsorption cycle A of the first adsorption unit has already been explained.
- the regeneration cycle R of the second adsorption unit 2 the latter or its adsorbent is heated by means of a suitable heating fluid or electrically, directly or indirectly, as previously explained.
- a gas stream f is obtained which can be carried out from the second adsorption unit 2.
- a flow through the corresponding adsorption unit 2 is carried out with material contact with the adsorbent, a corresponding gas flow f is continuously carried out here in a comparatively large volume; in the case of indirect heating, only a pressure rise is compensated, which results from the temperature expansion and the release of gas during the Desorption results.
- Part of the second gas mixture b here denoted by g, is introduced into the third adsorption unit 3, so that, as mentioned, a pressure in this adsorption unit 3 can be maintained in this way.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102018006960.6A DE102018006960A1 (de) | 2018-09-03 | 2018-09-03 | Verfahren zum Betreiben einer Temperaturwechseladsorptionsanlage und Temperaturwechseladsorptionsanlage |
PCT/EP2019/025274 WO2020048633A1 (de) | 2018-09-03 | 2019-08-20 | Verfahren zum betreiben einer temperaturwechseladsorptionsanlage und temperaturwechseladsorptionsanlage |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3846921A1 true EP3846921A1 (de) | 2021-07-14 |
EP3846921C0 EP3846921C0 (de) | 2024-05-01 |
EP3846921B1 EP3846921B1 (de) | 2024-05-01 |
Family
ID=67953732
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19768713.0A Active EP3846921B1 (de) | 2018-09-03 | 2019-08-20 | Verfahren zum betreiben einer temperaturwechseladsorptionsanlage und temperaturwechseladsorptionsanlage |
Country Status (5)
Country | Link |
---|---|
US (1) | US11806658B2 (de) |
EP (1) | EP3846921B1 (de) |
CA (1) | CA3111021A1 (de) |
DE (1) | DE102018006960A1 (de) |
WO (1) | WO2020048633A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111744318B (zh) * | 2020-06-30 | 2022-06-24 | 四川杰瑞恒日天然气工程有限公司 | 一种垃圾填埋气的臭气处理工艺 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030037672A1 (en) * | 2001-08-27 | 2003-02-27 | Shivaji Sircar | Rapid thermal swing adsorption |
EP1715938A4 (de) * | 2004-01-27 | 2008-08-06 | Purifics Environmental Technol | Fortschrittliches verfahren zur behandlung von verunreinigungen |
FR2911077B1 (fr) | 2007-01-05 | 2009-11-27 | Air Liquide | Procede de purification ou de separatiion utilisant plusieurs adsorbeurs decales en phase |
US8133302B2 (en) * | 2007-06-14 | 2012-03-13 | Exxonmobil Upstream Research Company | Process for purification of hydrocarbons |
EP3260185A1 (de) * | 2016-06-21 | 2017-12-27 | Donaldson Filtration Deutschland GmbH | Vorrichtung zur temperaturwechsel-adsorption und verfahren zur temperaturwechsel-adsorption für die reinigung von gasen |
EP3449996A1 (de) * | 2017-08-28 | 2019-03-06 | Casale Sa | Temperaturwechseladsorptionsverfahren |
EP3520881A1 (de) * | 2018-01-31 | 2019-08-07 | Linde Aktiengesellschaft | Verfahren zur trennung eines gasgemischstroms mittels temperaturwechseladsorption und temperaturwechseladsorptionsanlage |
-
2018
- 2018-09-03 DE DE102018006960.6A patent/DE102018006960A1/de not_active Withdrawn
-
2019
- 2019-08-20 CA CA3111021A patent/CA3111021A1/en active Pending
- 2019-08-20 WO PCT/EP2019/025274 patent/WO2020048633A1/de unknown
- 2019-08-20 EP EP19768713.0A patent/EP3846921B1/de active Active
- 2019-08-20 US US17/271,460 patent/US11806658B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
EP3846921C0 (de) | 2024-05-01 |
DE102018006960A1 (de) | 2020-03-05 |
US20210308615A1 (en) | 2021-10-07 |
US11806658B2 (en) | 2023-11-07 |
WO2020048633A1 (de) | 2020-03-12 |
CA3111021A1 (en) | 2020-03-12 |
EP3846921B1 (de) | 2024-05-01 |
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